Classifications

• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
  • C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
  • C01B39/28—Phillipsite or harmotome type

Definitions

• the invention describes the preparation of alkali metal aluminosilicates, in particular crystalline aluminosilicates having the P-structure. These materials are of value as a component in detergent formulations in which they remove calcium and magnesium hardness ions by ion exchange. They also have other properties which provide additional benefits when used in detergent formulations. These aluminosilicates will be referred to as zeolite P in this description.
• the zeolite P class includes a series of synthetic zeolite phases which may be in cubic configuration (also termed B or P c ) or tetragonal configuration (also termed P but is not limited to these forms.
• the structure and characteristics of the zeolite P class are given in "Zeolite Molecular Sieves" of Donald W Breck (published 1974 and 1984 by Robert E Krieger of Florida USA) .
• the zeolite P class has the typical oxide formula:
• M is an n-valent cation which for this invention is an alkali metal, that is lithium, potassium, sodium, caesium or rubidium with sodium and potassium being preferred and sodium being the cation normally used in commercial processes.
• sodium may be present as the major cation with another alkali metal present in a minor proportion to provide a specific benefit.
• EP-A-384,070 is disclosed a process for manufacturing zeolite P having a silicon to aluminium molar ratio not exceeding 1.33 wherein a sodium aluminate solution, having a Na 2 0:Al 2 0 3 molar ratio from 1.4 to 2.0, is mixed with a sodium silicate solution, having a Si0 2 :Na 2 0 molar ratio from 0.8 to 3.4, at a temperature from 25°C to boiling point and with vigorous stirring to give a gel having the following composition:
• the gel is then aged for 0.5 to 10 hours at a temperature above 70°C, the crystalline sodium aluminosilicate thus formed being then washed and dried.
• EP-A-565,364 is disclosed a process for industrial production of P zeolite having the oxide formula
• y is the water content, comprising the steps of: i. a sodium aluminate solution having a temperature of at least 25°C is mixed with a sodium silicate solution at a temperature of at least 25°C in a stirred vessel in the presence of a slurry of P zeolite seed to form a gel having the composition,
• A1 2 0 3 (1-3.5) (preferably 1.80-2.2)Si0 2 : (1.2-7.5) (preferably 1.5-5)Na 2 0: (25 to 450) (preferably 40 to 150) H 2 0
• the invention relates to a process for manufacturing an alkali metal aluminosilicate of zeolite P type having the oxide formula
• reacting zone it is understood a reacting vessel or a zone of a plug flow reactor as for example marketed by Power Fluidics, AEA Technology, Risley, Warrington, U.K..
• the mixture obtained in the first reacting zone by adding together a sodium silicate solution and a sodium aluminate solution in the presence of zeolite P seeds has a Si0 2 /Al 2 0 3 mole ratio of more than 2.2 and, in the second reacting zone, a second sodium aluminate solution is added so as to give an overall Si0 2 /Al 2 0 3 mole ratio of less than 2.2 and a H 2 0/A1 2 0 3 mole ratio of less than 150 .
• dilute alkaline solution (8.1% Na 2 0) was placed in a 15 litre baffled flask. The solution was stirred (600rpm) and heated to 95°C. To the stirred solution, dilute silicate solution (14.7% Si0 2 , 9.4% Na 2 0, 1% w/w of zeolite P seeds), preheated at 90°C, and dilute aluminate solution (9.13% Al 2 0 3 , 12.5% Na 2 0) were simultaneously added at identical rate of 40g/minute. The zeolite P seeds in the dilute silicate solution were produced as disclosed in EP-A- 565,364.
• the dried samples were analyzed by XRD and all the samples were crystalline zeolite P.
• example 1 The procedure of example 1 was repeated except that 3 reactor pots were employed instead of 2. Samples were taken from the outlet pipe, filtered, washed an dried on an hourly basis. This continuous operation was maintained for 6 hours. The dried samples were also crystalline zeolite P.
• Example 3 The procedure of Example 3 was repeated with suitable increase in the A1 2 0 3 concentration in the aluminate stream so as to obtain a gel composition with Si0 2 /Al 2 0 3 ratio of 2.0 instead of 2.7.

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• Chemical & Material Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Geology (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Materials Engineering (AREA)
• Inorganic Chemistry (AREA)
• Silicates, Zeolites, And Molecular Sieves (AREA)
• Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
• Solid-Sorbent Or Filter-Aiding Compositions (AREA)

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• 1994
  • 1994-11-07 GB GB9422401A patent/GB9422401D0/en active Pending
• 1995
  • 1995-10-24 WO PCT/EP1995/004195 patent/WO1996014270A1/en active IP Right Grant
  • 1995-10-24 DE DE69506440T patent/DE69506440T2/de not_active Expired - Fee Related
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  • 1995-10-24 KR KR1019970702996A patent/KR100391869B1/ko not_active IP Right Cessation
  • 1995-10-24 ES ES95936550T patent/ES2125669T3/es not_active Expired - Lifetime
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  • 1995-10-24 AU AU38446/95A patent/AU3844695A/en not_active Abandoned
• 1999
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